JP2006043626A - Water treatment apparatus - Google Patents

Water treatment apparatus Download PDF

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Publication number
JP2006043626A
JP2006043626A JP2004230370A JP2004230370A JP2006043626A JP 2006043626 A JP2006043626 A JP 2006043626A JP 2004230370 A JP2004230370 A JP 2004230370A JP 2004230370 A JP2004230370 A JP 2004230370A JP 2006043626 A JP2006043626 A JP 2006043626A
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sewage
stirring
container
water
flocculant
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Katsumi Hara
勝美 原
Kenichiro Hara
健一郎 原
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HARA GIKEN KOGYO KK
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HARA GIKEN KOGYO KK
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Abstract

<P>PROBLEM TO BE SOLVED: To provide a high power, highly capacity, and compact-sized water treatment apparatus. <P>SOLUTION: The water treatment apparatus comprises a mixing container for mixing a continuously supplied flocculant and polluted water, a stirring container for stirring the mixed polluted water by water current, a flocculating container for flocculating the stirred polluted water, a flocculating and precipitating tank containing the flocculating container and flocculating and precipitating the primarily treated water discharged out of the flocculating container, a filtrating tank for filtrating the secondarily treated water overflowing the flocculating and precipitating tank and discharged out of the tank and whose filtration capability is recovered by washing the filtration layer by introducing air from outside when the filtration capability is decreased. <P>COPYRIGHT: (C)2006,JPO&NCIPI

Description

本発明は、凝集剤を用いて汚水中の汚物を凝集、沈殿させる水処理装置に関するものである。 The present invention relates to a water treatment apparatus for aggregating and precipitating filth in wastewater using a flocculant.

従来、水処理装置としては活性汚泥法やフィルターを用いて汚物を分離するもの等が採用されている。一方、近年では高分子凝集剤やゼオライト系の凝集剤が開発されている。それらを汚水に投入し急速攪拌することで汚物の凝集、沈殿させ水処理をすることが可能である。 Conventionally, as the water treatment apparatus, an activated sludge method or a device for separating filth using a filter has been adopted. On the other hand, in recent years, polymer flocculants and zeolite flocculants have been developed. By putting them into sewage and stirring rapidly, it is possible to agglomerate and precipitate the sewage to treat the water.

しかし、これらの凝集剤を用いて効率よく、しかも処理水量の大きな水処理装置の開発はなされていない。検討したところ、以下の点が解決すべき課題である。第一に、本発明で使用する無機系高分子凝集剤は7秒から12秒で急速混合攪拌する必要があること。第二にこの凝集剤は機械攪拌を行うと凝集物を砕いてしまうこと。第三に攪拌された凝集剤と汚水を効率的に凝集沈殿させる必要があること。 However, a water treatment apparatus that uses these flocculants efficiently and has a large amount of treated water has not been developed. After examination, the following points are issues to be solved. First, the inorganic polymer flocculant used in the present invention needs to be rapidly mixed and stirred in 7 to 12 seconds. Second, the flocculant breaks up the aggregates when mechanically stirred. Third, it is necessary to efficiently coagulate and precipitate the agglomerated agent and sewage that have been stirred.

これらの課題を解決し、効率がよく、処理能力が大きく、コンパクトな水処理装置を提供することを目的とする。 An object of the present invention is to provide a compact water treatment apparatus that solves these problems, is efficient, has a large treatment capacity, and is compact.

本発明の水処理装置は、凝集剤投入機から連続的に投入される凝集剤と外部から導入される汚水とを混和する混和容器と、混和された汚水を水流を利用して急速攪拌する攪拌容器と、前記攪拌容器により急速攪拌された汚水を導入し渦流によって緩速攪拌することで凝集物をより大きく形成させる凝集形成容器と、凝集された凝集物を沈殿させる凝集沈殿槽と、前記凝集沈殿槽より浮上流出した、汚水中の汚物を濾過層の中で付着させ濾過した濾過水を排出する濾過槽と、を有することで上記問題点を解決したものである。 The water treatment apparatus of the present invention comprises a mixing vessel for mixing a flocculant continuously fed from a flocculant charging machine and wastewater introduced from the outside, and stirring for rapidly stirring the mixed wastewater using a water flow. A container, an agglomeration forming container for forming agglomerates larger by introducing sewage water rapidly stirred by the stirring vessel and slowly stirring by vortex, agglomeration settling tank for precipitating the agglomerated aggregates, and the agglomeration The present invention solves the above-mentioned problems by having a filtration tank that discharges the filtered water that is attached to the filth in the sewage that floats and flows out of the settling tank in the filtration layer.

本発明は、食品排水、工場排水、高濁度処理、雑排水、池、沼、湖の水質改善に幅広く使用できる。 INDUSTRIAL APPLICABILITY The present invention can be widely used for improving water quality of food wastewater, factory wastewater, high turbidity treatment, miscellaneous wastewater, ponds, swamps, and lakes.

本発明は広大な設置場所を必要としないため、ダム及びトンネル工事等における高濁度水処理で、従来の装置は巨大な装置を使用するため広大な土地を必要としていたが、本発明を使用することで設置場所の軽減ができる。また、都会などの狭い工事現場でも装置が小型なため設置可能である。 Since the present invention does not require a vast installation site, it is a high turbidity water treatment in dams and tunnel constructions, etc., and the conventional device used a huge device, but it requires a vast land, but the present invention is used. By doing so, the installation location can be reduced. It can also be installed in small construction sites such as urban areas due to its small size.

本発明は、食品排水、工場排水、高濁度処理、雑排水に使用できるため、業務拡張等により、既設設備の増設を必要とする場合にも排水設備を増設せずに本装置を設置することにより処理能力を向上することが可能である。 Since the present invention can be used for food wastewater, factory wastewater, high turbidity treatment, and miscellaneous wastewater, even if it is necessary to expand existing facilities due to business expansion, etc., this device is installed without adding drainage facilities. Therefore, it is possible to improve the processing capacity.

この装置の濾過層洗浄方式は通常の濾過層の洗浄と違い洗浄水を必要とせず、また洗浄排水が出ないという利点がある。 The filtration layer cleaning system of this apparatus has the advantage that it does not require cleaning water unlike normal filter layer cleaning, and does not generate cleaning waste water.

本発明を実施するための最良の形態BEST MODE FOR CARRYING OUT THE INVENTION

この水処理装置は大きく分けると、凝集剤投入器、混和容器、攪拌容器、凝集沈澱槽、濾過槽、とで構成されている。 This water treatment apparatus is roughly divided into a flocculant charging device, a mixing vessel, a stirring vessel, a coagulating sedimentation tank, and a filtration tank.

つぎに、本発明の実施の形態を図面を参照しながら詳細に説明する。 Next, embodiments of the present invention will be described in detail with reference to the drawings.

図1に水処理装置のシステム全体の構成を示す。 Fig. 1 shows the overall configuration of the water treatment system.

凝集剤投入器2は、粉末凝集剤を使用するとき、粉末用凝集投入器を、又液体用凝集剤を使用するときは、液体用凝集剤注入ポンプを、使用する。外部から導入される汚水と凝集剤投入器から連続的に添加される凝集剤とを効率よく混合する為、混和容器の上部より凝集剤を連続的に添加する。 The flocculant charging device 2 uses a powder flocculant charging device when using a powder flocculant, and a liquid flocculant injection pump when using a liquid flocculant. In order to efficiently mix the waste water introduced from the outside and the flocculant continuously added from the flocculant feeder, the flocculant is continuously added from the upper part of the mixing vessel.

混和容器3の側面には汚水の導水管1が接続されている。導水管1から加圧された汚水が混和容器3に導入されると、汚水は混和容器3の内壁に沿って渦流を形成しながら落下する。この渦流の中に凝集剤投入器2から凝集剤が連続的に添加されるので、汚水と凝集剤は攪拌され混和容器3の底部の穴を通じて攪拌容器4の最上部に設けられた攪拌板10上に案内される。 A sewage water conduit 1 is connected to the side surface of the mixing vessel 3. When the pressurized sewage from the water conduit 1 is introduced into the mixing vessel 3, the sewage falls along the inner wall of the mixing vessel 3 while forming a vortex. Since the flocculant is continuously added from the flocculant feeder 2 into this vortex, the sewage and the flocculant are stirred and the stirring plate 10 provided at the top of the stirring vessel 4 through the hole at the bottom of the mixing vessel 3. Guided up.

図2は攪拌容器4の詳細な構造を示す。攪拌容器4の内壁には6から8枚の攪拌板が水平方向に連設され、6から8枚の攪拌板は攪拌容器の一方の内壁に固定され、反対の内壁との間に汚泥が堆積することなく落下できる程度の隙間が生じるように、交互に取り付けられる。又、攪拌板の奇数1、3、5、7段目の板10は、平板のみを固定し、攪拌板の偶数2、4、6、8段目の板11には、平板11の上に垂直に数箇所平板12を固定する。そして、凝集剤を含んだ汚水はこの攪拌板の奇数1段目の板10上を流れて攪拌容器4の内壁に衝突し、下方の、攪拌板の偶数2段目の板11に落ちて、平板11の上に垂直に固定された平板12に激しく衝突を数回繰り返して、攪拌容器4内壁に衝突しながら、凝集剤を含んだ汚水は、下方の、3段目の攪拌板である平板10上を加速して流れる。こうして、攪拌と加速を繰り返すことで凝集剤を含んだ汚水を十分に混合し、攪拌容器4の底部に設けられた汚水出口14から導水管5を通って、凝集沈澱槽7に導入される。 FIG. 2 shows the detailed structure of the stirring vessel 4. 6 to 8 stirring plates are connected to the inner wall of the stirring vessel 4 in the horizontal direction, the 6 to 8 stirring plates are fixed to one inner wall of the stirring vessel, and sludge is deposited between the opposite inner walls. It is attached alternately so that a gap that can be dropped without causing a gap is generated. Further, the odd-numbered first, third, fifth and seventh stage plates 10 of the stirring plate are fixed only on the flat plate, and the even-numbered second, fourth, sixth and eighth stage plates 11 are placed on the flat plate 11. Several flat plates 12 are fixed vertically. And the sewage containing the flocculant flows on the odd-numbered first-stage plate 10 of this stirring plate, collides with the inner wall of the stirring vessel 4, falls to the lower even-numbered second-stage plate 11 of the stirring plate, While colliding violently with the flat plate 12 vertically fixed on the flat plate 11 several times and colliding with the inner wall of the stirring vessel 4, the sewage containing the flocculant is a flat plate which is the lower third stage stirring plate. It accelerates on 10 and flows. Thus, the sewage containing the flocculant is sufficiently mixed by repeating the stirring and acceleration, and introduced into the flocculation / sedimentation tank 7 from the sewage outlet 14 provided at the bottom of the stirring vessel 4 through the water conduit 5.

この攪拌容器4で外部より導入される加圧された汚水を十分に攪拌させるためには、攪拌容器内の空気を外部に放出する必要がある。そのための配管を攪拌容器4の底部より配管13を立ち上げ混合容器よりも高い位置で大気開放する。 In order to sufficiently stir the pressurized sewage introduced from the outside in the stirring vessel 4, it is necessary to release the air in the stirring vessel to the outside. For this purpose, the piping 13 is raised from the bottom of the stirring vessel 4 and opened to the atmosphere at a position higher than the mixing vessel.

そして、図4では凝集沈殿槽7の詳細な構造を示す。凝集沈澱槽7は凝集剤によって凝集された汚水中の汚物を沈澱させるものであるが、攪拌容器4の底部に設けられた汚水出口14から導水管5を通って凝集沈澱槽7内部に設置された円筒体である凝集形成容器6に、攪拌容器4で、凝集剤と汚水を十分に混合されたものが導水管5を通って流入する。 FIG. 4 shows the detailed structure of the coagulation sedimentation tank 7. The coagulation sedimentation tank 7 precipitates filth in the sewage water aggregated by the coagulant. The coagulation sedimentation tank 7 is installed in the coagulation sedimentation tank 7 from the sewage outlet 14 provided at the bottom of the stirring vessel 4 through the water conduit 5. In the agglomeration container 6 which is a cylindrical body, the agitation container 4 in which the flocculant and sewage are sufficiently mixed flows through the water conduit 5.

図3では凝集形成容器6の詳細な構造を示す。本装置使用の凝集剤は急速攪拌後に緩速攪拌をすることにより凝集効果が高く得られることから、前記凝集形成容器6内部上方には、螺旋状板16が、数段取付けられており凝集剤と汚水を十分に急速攪拌されたものが、螺旋状板16を取り付けることにより、ゆっくり旋回しながら下方に落ち、旋回することにより凝集効果を高め、凝集形成容器6に設けた螺旋状板16を通過した後、円筒体下方で旋回力を維持しながら円筒体の底部より汚水中の汚物を集結し、より大きな凝集物として凝集沈澱槽7の底部にすばやく沈澱させる。 FIG. 3 shows the detailed structure of the agglomeration container 6. Since the flocculant used in this apparatus has a high agglomeration effect by stirring slowly after rapid stirring, several stages of spiral plates 16 are attached above the inside of the agglomeration forming container 6. When the sewage is sufficiently stirred rapidly, the spiral plate 16 is attached to the sewage and falls downward while slowly turning. After passing, the filth in the sewage is collected from the bottom of the cylinder while maintaining the turning force below the cylinder, and quickly settled as a larger agglomerate on the bottom of the aggregation sedimentation tank 7.

凝集形成容器6は凝集沈殿槽7内に埋没されており水圧の負荷により水流速度を制限し、また凝集沈殿槽7の容量を従来よりも小さく作ることができる効果も持つものである。 The agglomeration vessel 6 is buried in the agglomeration sedimentation tank 7 and has an effect of limiting the water flow speed by the load of water pressure and making the capacity of the agglomeration sedimentation tank 7 smaller than the conventional one.

汚水中の汚物を、攪拌容器4及び凝集形成容器6にて凝集した汚水は、集結された汚物と、処理された一次処理水とに、分離される。 The sewage obtained by aggregating the sewage in the sewage in the agitation container 4 and the agglomeration container 6 is separated into the collected sewage and the treated primary treated water.

凝集形成容器下部17より凝集沈澱槽7内に拡散された一次処理水は、上昇水流で凝集沈澱槽7の上部に設けた越流堰18より上澄み水が越流する。 The primary treated water diffused into the coagulation sedimentation tank 7 from the lower part 17 of the coagulation formation vessel overflows the supernatant water from the overflow weir 18 provided in the upper part of the coagulation sedimentation tank 7 by the rising water flow.

螺旋板16を通過した一次処理水は、大きな凝集物と微細な凝集物が形成され、大きな凝集物は凝集沈澱槽7の底部に沈澱堆積し、微細な凝集物は上昇水流に乗り凝集沈殿槽7の上部に設けた越流堰18よりオーバーフローする。これを二次処理水とし、この二次処理水が下方に隣接する濾過槽8に、滝のように落下する。 The primary treated water that has passed through the spiral plate 16 is formed with large aggregates and fine aggregates. The large aggregates are deposited on the bottom of the aggregation sedimentation tank 7, and the fine aggregates ride on the rising water flow and accumulate in the aggregation sedimentation tank. The overflow overflows from the overflow weir 18 provided at the top of 7. This is treated as secondary treated water, and the secondary treated water falls like a waterfall into the filtration tank 8 adjacent below.

図5及び図6では濾過槽8の詳細な構造を示す。濾過槽8は、凝集沈殿槽7よりオーバーフローして滝のように落下した二次処理水が仕切り板20の下部を潜り抜け多孔板21を通過し濾過槽8内に導入された2次処理水を濾過層22の下から上に通して濾過するものである。 5 and 6 show the detailed structure of the filtration tank 8. In the filtration tank 8, the secondary treated water that overflows from the coagulation sedimentation tank 7 and falls like a waterfall passes through the lower part of the partition plate 20, passes through the porous plate 21, and is introduced into the filtered tank 8. Is filtered through the filter layer 22 from the bottom to the top.

この濾過層22は、プラスチック製 タテ5cm×ヨコ5cm×厚み1mmの網目状で水中において浮力のある物質を濾過材31とし、これを濾過槽8内に20cmの厚さに積層する。2次処理水がこの濾過層中の濾過材31に付着されることで濾過がなされる。また、濾過槽8内の濾過層22の下方には多数の気泡を発生させる散気管9が設けられ、気泡が濾過層22の片側に当てられるように構成されている。この散気管9には、外部より空気が供給されており、これにより濾過層22の濾過材31を濾過槽8内で強制的に対流させる。この対流により濾過材31に付着した微細な凝集物等を剥離させ洗浄する。この洗浄によって、濾過層22の能力が付着物の増加に伴い低下したときに外部より空気を供給することで能力が回復し再び濾過状態に戻す。 This filtration layer 22 is a plastic vertical 5 cm × width 5 cm × thickness 1 mm mesh, and a substance having buoyancy in water is used as the filter medium 31, and this is laminated in the filtration tank 8 to a thickness of 20 cm. Filtration is performed by adhering the secondary treated water to the filter medium 31 in the filter layer. Further, an air diffuser 9 that generates a large number of bubbles is provided below the filtration layer 22 in the filtration tank 8, and the bubbles are configured to be applied to one side of the filtration layer 22. Air is supplied to the air diffuser 9 from the outside, so that the filter medium 31 of the filter layer 22 is forcibly convected in the filter tank 8. By this convection, fine aggregates and the like adhering to the filter medium 31 are peeled off and washed. By this cleaning, when the ability of the filtration layer 22 decreases with the increase in the amount of deposits, the ability is recovered by supplying air from the outside, and the filtration state is restored.

凝集沈殿槽7の底には排出配管26とバルブ25がもうけられておりバルブ25を開くことで凝集沈殿槽7内に体積した汚物を排出可能である。また、濾過槽8の底には排出配管28、30が設けられており排出配管28に接続されたバルブ27を開くと多孔版21で仕切られた凝集沈殿槽7側の場所の汚物を、排出配管30に接続されたバルブ29を開くと濾過層22の下部にたまった汚物を、排出することができる。 A discharge pipe 26 and a valve 25 are provided at the bottom of the coagulation sedimentation tank 7, and by opening the valve 25, the filth that has accumulated in the coagulation sedimentation tank 7 can be discharged. Further, discharge pipes 28 and 30 are provided at the bottom of the filtration tank 8. When the valve 27 connected to the discharge pipe 28 is opened, the filth in the place on the coagulation sedimentation tank 7 side partitioned by the perforated plate 21 is discharged. When the valve 29 connected to the pipe 30 is opened, the filth accumulated in the lower portion of the filtration layer 22 can be discharged.

本発明の実施形態に係わる水処理装置のシステム構成を示す図である。It is a figure which shows the system configuration | structure of the water treatment apparatus concerning embodiment of this invention. 攪拌容器の断面図である。It is sectional drawing of a stirring container. 凝集形成容器の側面図である。It is a side view of an aggregation formation container. 凝集沈殿槽の側面図である。It is a side view of a coagulation sedimentation tank. 凝集沈殿槽の平面図である。It is a top view of a coagulation sedimentation tank. 濾過槽の断面図である。It is sectional drawing of a filtration tank. 濾過材の平面図である。It is a top view of a filter medium. A−A断面図である。It is AA sectional drawing.

符号の説明Explanation of symbols

1 導水管 2 凝集剤投入機 3 混和容器
4 攪拌容器 5 導水管 6 凝集形成容器
7 凝集沈殿槽 8 濾過槽 9 散気管
10 攪拌板 11 攪拌板 12 攪拌板
13 空気逃し管 14 汚水出口 15 導入口
16 螺旋状板 17 凝集形成容器出口 18 越流堰
19 凝集沈殿槽出口 20 仕切り板 21 多孔版
22 濾過層 23 越流堰 24 濾過層出口
25 バルブ 26 排出配管 27 バルブ
28 排出配管 29 バルブ 30 排出配管
31 濾過材
DESCRIPTION OF SYMBOLS 1 Water guide pipe 2 Coagulant injection machine 3 Mixing container 4 Stirring container 5 Water guide pipe 6 Aggregation formation container 7 Coagulation sedimentation tank 8 Filtration tank 9 Aeration pipe 10 Stirring plate 11 Stirring plate 12 Stirring plate 13 Air escape pipe 14 Sewage outlet 15 Inlet 16 Spiral plate 17 Agglomeration forming container outlet 18 Overflow weir 19 Coagulation sedimentation tank outlet 20 Partition plate 21 Porous plate 22 Filtration layer 23 Overflow weir 24 Filtration layer outlet 25 Valve 26 Discharge piping 27 Valve 28 Discharge piping 29 Valve 30 Discharge piping 31 Filter media

Claims (4)

凝集剤投入機より投入される凝集剤と外部から導入される汚水とを混和する混和容器と、混和容器により混和された汚水を導入し攪拌する攪拌容器と、それにより攪拌された汚水を導入し、汚れを凝集形成させる凝集形成容器と、凝集された汚物を凝集沈殿させる凝集沈殿槽と、前記凝集沈殿槽にて処理された凝集物を濾過した水を排出する濾過槽と、を有する水処理装置。 A mixing container for mixing the flocculant introduced from the flocculant charging machine and the sewage introduced from the outside, a stirring container for introducing and stirring the sewage mixed by the mixing container, and the sewage stirred thereby are introduced. A water treatment comprising: an agglomeration container for agglomerating and forming a soil; an agglomeration sedimentation tank for aggregating and sedimenting the agglomerated waste; and a filtration tank for discharging water obtained by filtering the agglomerate treated in the agglomeration sedimentation tank. apparatus. 前記攪拌容器は外部から汚水導入部と凝集剤導入部を有する混和容器から導入される汚水を攪拌するための複数の攪拌板を縦横に組み合わせ連結された攪拌部、及び攪拌された汚水と凝集剤を排出するために設けた排水口を有する攪拌容器を有することを特徴とする請求項1記載の水処理装置。 The stirring vessel is a stirring portion in which a plurality of stirring plates for stirring sewage introduced from a mixing vessel having a sewage introduction portion and a flocculant introduction portion from the outside are combined and connected, and the stirred sewage and the flocculant. The water treatment apparatus according to claim 1, further comprising a stirring vessel having a drain port provided for discharging water. 前記凝集沈殿槽は、円筒状内に複数の螺旋状板を連設することにより渦流をつくり下部に設けた排水口から排出される凝集形成容器と、前記凝集形成容器下部より導入される汚水を底部に沈殿させ、汚水を凝集沈殿槽上部より越流する越流壁と、越流した汚水を排出する排水口と、を有することを特徴とする請求項1の水処理装置。 The agglomeration sedimentation tank comprises a coagulation formation container that is vortexed by connecting a plurality of spiral plates in a cylindrical shape and discharged from a drain outlet provided in the lower part, and sewage introduced from the lower part of the aggregation formation container. The water treatment device according to claim 1, further comprising an overflow wall for precipitating at the bottom and overflowing sewage from the upper part of the coagulation sedimentation tank, and a drain outlet for discharging the overflowed sewage. 前記濾過槽は、空気を導入することで使用と共に低下する濾材の能力を回復させる機能を有することを特徴とする請求項1記載の水処理装置。 The water treatment apparatus according to claim 1, wherein the filtration tank has a function of recovering the ability of the filter medium that decreases with use by introducing air.
JP2004230370A 2004-08-06 2004-08-06 Water treatment apparatus Pending JP2006043626A (en)

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JP2009000670A (en) * 2007-06-22 2009-01-08 Nippon Solid Co Ltd Treatment method of raw water
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JP2013049057A (en) * 2012-11-05 2013-03-14 Toshiba Corp Solid-liquid separation system
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JP2014140845A (en) * 2014-03-31 2014-08-07 Toshiba Corp Solid-liquid separation system
CN109761400A (en) * 2019-03-11 2019-05-17 郭淑梅 A kind of water purification installation in sewage treatment
CN114436450A (en) * 2022-02-24 2022-05-06 闫俊飞 Sewage filtering device for hydraulic engineering

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JP2006181400A (en) * 2004-12-24 2006-07-13 Okumura Corp Muddy water treatment apparatus
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JP2011083709A (en) * 2009-10-15 2011-04-28 Toshiba Corp Solid-liquid separation system
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KR101404065B1 (en) 2012-08-23 2014-06-05 주식회사 에스비씨환경건설 Different Impellers Type Settling Tank(DIST)
JP2013049057A (en) * 2012-11-05 2013-03-14 Toshiba Corp Solid-liquid separation system
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CN109761400A (en) * 2019-03-11 2019-05-17 郭淑梅 A kind of water purification installation in sewage treatment
CN114436450A (en) * 2022-02-24 2022-05-06 闫俊飞 Sewage filtering device for hydraulic engineering

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